“…Recently, a great deal of research has been devoted to the leaching process of waste Li-ion battery scraps with different types of mineral acids like HCl (Guo et al, 2016), H3PO4 (Chen et al, 2017), H2SO4 (Pagnanelli et al, 2016) and organic acids including citric acid (Zheng et al, 2016), malic acid (Li et al, 2010) and lactic acid (Li et al, 2017). Moreover, the leaching efficiency of cobalt and lithium has also been shown to increase with the use of additional reducing agents like H2O2 (Pagnanelli et al, 2017b), Na2S2O5 (Vieceli et al, 2018), NaHSO3 (Meshram et al, 2016), D-glucose (Granata et al, 2012) as well as ascorbic acid (Li et al, 2012). (Meshram et al, 2016) 35.8 a 1 M H2SO4 + 5% (v/v) H2O2 50 14.1 3.1 79 94 - (Meshram et al, 2016) 44.2 a 4 M H2SO4 + 10% (v/v) H2O2 100 42.0 5.3 95 96 - (Chen et al, 2011) 54.0 a 2 M H2SO4 + 5% (v/v) H2O2 50 26.7 3.2 99 99 - (Sun and Qiu, 2011a) 35.8 a 1 M H2SO4 + 7.5 M NaHSO3 50 15.2 3.0 85 93 - (Meshram et al, 2016) 35.4 a 3 M H2SO4 + 0.25 M Na2S2O3 66 23.1 2.4 99 99 50 (Wang et al, 2012) 41.5 a 0.34 M H3PO4 + 2% (v/v) H2O2 8 3.2 0.4 95 95 - (Pinna et al, 2017) 54.0 a 0.1 M Citric + 0.02 M ascorbic 2 0.9 0.1 80 100 - (Nayaka et al, 2015) 54.0 a 0.5 M glycine + 0.02 M ascorbic 2 1.0 0.1 95 95 - (Nayaka et al, 2016a) 55.0 a 1.25 M ascorbic acid 25 13.1 1.6 95 99 - (Li et al, 2012) -2 M H2SO4 + 4% H2O2 66 32.7 2.3 97 97 65 (Nayl et al, 2017) 52.0 a 1 M H2SO4 + 0.02 M glucose 35 16.0 1.5 88 92…”